EP0116512A1 - Composition déliante pour fibres comprenant un composé diamido-ammonium quaternaire et un acide gras alkoxylé - Google Patents

Composition déliante pour fibres comprenant un composé diamido-ammonium quaternaire et un acide gras alkoxylé Download PDF

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Publication number
EP0116512A1
EP0116512A1 EP84630017A EP84630017A EP0116512A1 EP 0116512 A1 EP0116512 A1 EP 0116512A1 EP 84630017 A EP84630017 A EP 84630017A EP 84630017 A EP84630017 A EP 84630017A EP 0116512 A1 EP0116512 A1 EP 0116512A1
Authority
EP
European Patent Office
Prior art keywords
fatty acid
formulation
fatty alcohol
debonding
cellulose fiber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP84630017A
Other languages
German (de)
English (en)
Inventor
William John Zeman
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Witco Corp
Original Assignee
Sherex Chemical Co Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sherex Chemical Co Inc filed Critical Sherex Chemical Co Inc
Publication of EP0116512A1 publication Critical patent/EP0116512A1/fr
Withdrawn legal-status Critical Current

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Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/001Modification of pulp properties
    • D21C9/002Modification of pulp properties by chemical means; preparation of dewatered pulp, e.g. in sheet or bulk form, containing special additives
    • D21C9/005Modification of pulp properties by chemical means; preparation of dewatered pulp, e.g. in sheet or bulk form, containing special additives organic compounds

Definitions

  • the present invention relates to paper debonders and more particularly to a novel paper or fiber debonding formulation.
  • tissue debonder reduces the tensile strength of the tissue by weakening the cellulosic fiber-to-fiber bond. Desirably, the ability of the tissue to absorb moisture is not adversely effected by the paper debonder.
  • paper debonders are being employed in two consumer product lines.
  • One line is the disposable tissue (facial and bathroom) product line where debonders are added to the pulp slurry in the wet end of the tissue manufacturing operation.
  • the debonders are expected to provide a finished tissue of improved softness.
  • Disposable diapers are the second consumer product line employing debonders and their use is somewhat different than the use of debonders in disposable tissue production.
  • the paper debonder is added to the pulp slurry at the wet end of the disposable diaper manufacturing operation (ie. at the same manufacturing juncture as in the disposable tissue manufacturing operation), but the debonder functions as a processing aid to assist in the fluffing of the finished paper sheet into the bulky diaper sheeting.
  • the reduced tensile strength of the pulp fibers thus, aids mechanical pickers in fluffing the dried pulp into a bulky sheeting which is soft yet retains excellent water absorbency.
  • the present invention is directed to a novel fiber debonding formulation which is not only effective in reducing the cellulosic fiber-to-fiber bond, but also is non-toxic and safe (very low eye and skin irritation).
  • the present invention is a method for treating cellulosic pulp fibers to reduce interfiber bonding and to reduce the mechanical strength of webs formed therefrom.
  • the method is characterized by blending with an aqueous cellulosic pulp slurry a debonding formulation comprising:
  • the resulting debonded cellulosic fiber pulp web possessing reduced interfiber bonding and reduced mechanical strength results from the foregoing method and additionally comprises an aspect of the present invention.
  • Advantages of the present invention include the excellent performance imparted by the paper debonders of the present invention in reducing interfiber bonding and reducing mechanical strength for providing fluffy webs of treated pulp which webs or sheets additionally possess excellent moisture absorbency characteristics. Another advantage is that the ingredients of the debonder formulation are non-toxic and are non-irritants. A further advantage is the debonding formulation is fluid at room temperature and is easily handleable by the fluffed pulp or tissue manufacturer.
  • alkoxylated fatty acids or fatty alcohols employed in the debonding formulation of the present invention traditionally have not been recognized as effective paper debonders themselves.
  • the disclosed quaternary ammonium compounds and alkoxylated fatty acids or fatty alcohols provide a unique (synergistic) fiber debonding formulation which is extremely effective and its effectiveness is quite unexpected based upon the prior art.
  • such quaternary amido ammonium compounds can be represented by the general formula :
  • R will comprise a CS-C 30 aliphatic group and preferably such groups are hydrocarbyl (fatty) groups. It must be recognized, however, that the occasional presence of oxygen or nitrogen in such substituents may be encountered and their presence is permissible provided that the resulting quaternary ammonium compound in combination with the alkoxylated fatty acid will provide a debonding formulation which possesses the requisite fluidity for use as a paper debonder at commercial scale operations.
  • R1 is a C 12 -C 18 aliphatic group typically being a fatty group derived from natural and synthetic fatty acids.
  • R 2 comprises a (polyoxy alkylene) hydroxy alkyl group which results from the alkoxylation of the amine nitrogen to which it is attached. Desirably, R 2 will result from the ethoxylation or propoxylation of the amine nitrogen to which it is attached.
  • R3 preferably is a C l -C 4 alkyl group and results from the conventional alkylation of a tertiary amine for forming a quaternary ammonium compound.
  • X is a monovalent anion typically encountered in the formation of quaternary ammonium compounds and most often will be halogen, nitrate, acetate, hydroxide, sulfate, or the like though chlorine and sulfate are the most prevelant.
  • Synthesis of the quaternary ammonium compounds is based upon diethylene triamine (2,2'-diaminodiethylamine).
  • the diethylene triamine molecule is reacted with a C 8 -C 30 carboxylic acid for forming amide groups.
  • carboxylic or fatty acids gives rise to the R l substituent.
  • the resulting diamidoamine then is alkoxylated in conventional fashion and to such an extent that essentially a 100 percent tertiary amine contentresults in the reaction mixture. While theoretically only about one mole of alkylene oxide is required for this reaction, generally an excess, eg. up to 50 percent, will be used to ensure the tertiary amine content requirement.
  • ethylene oxide and propylene oxide are the reactants of choice and will result in formation of the R 2 substituent.
  • the diamido tertiary amine molecule is alkylated in conventional fashion to form the resulting quaternary ammonium structure.
  • Alkyl halogens, alkyl nitrates, alkyl sulfates, etc. will be used for this reaction in conventional fashion and will result in the R 3 substituent and the X monovalent anion.
  • the resulting quaternary ammonium compound can be cut in an alcohol, glycol, or similar solvent for increasing its handling characteristics and/or to supply a desired actives concentration of the quaternary ammonium compound for formulating the debonder formulation of the present invention.
  • the proportion of quaternary ammonium compound in the ultimate debonding formulation generally will be from between about 10% or 50% by weight of the debonding formulation.
  • the fatty acids or alcohols are conventional in nature broadly ranging from C S -C 30 fatty acids or alcohols, advantageously C 12 -C 22 and preferably C 18 fatty acids or alcohols.
  • the fatty acids or alcohols are alkoxylated in conventional fashion, advantageously with ethylene oxide, though propylene oxide, butylene oxide, and other conventional alkylene oxides may be used in this reaction scheme.
  • the proportion of alkoxy groups generally should be from between about 2 and 12 moles of alkoxy group per mole of fatty acid or alcohol and advantageously from between about 4 and 7 moles per mole of fatty acid or alcohol.
  • the proportion of alkoxylated fatty acid or alcohol in the debonding formulation will range from between about 90% to 50% by weight of the debonding formulation.
  • the debonding formulation optionally may contain minor proportions of solvents for improving the fluidity and handling characteristics of the debonding formulation.
  • solvents for improving the fluidity and handling characteristics of the debonding formulation.
  • propylene glycol orthe like may be used in the debonding formulation for improving handling characteristics of the debonding formulation without imparting any adverse effects to the debonded pulp.
  • Additional such fluidity-improving solvents include, for example, alkanols, other alkyleneglycols, ethers and the like.
  • the proportion of alkoxylated fatty acid or alcohol is rediced to accommodate such solvents for providing between about 40 and 60weight percent alkoxylated fatty acid or alcohol and between about 5 and 20 percent fluidity-enhancing solvent.
  • the debonding formulation is manufactured readily by mechanical blending of the quaternary ammonium compound and alkoxylated fatty acid or fatty alcohol in conventional fashion, optionally also containing a fluidity-enhancing solvent.
  • the debonding formulation is applied to an aqueous pulp slurry in conventional fashion.
  • the type of pulp employed is not a limitation on use of the debonding formulations and can be conventional Kraft pulp or sulfitepulp.
  • the debonding formulation is added to the aqueous slurry in a proportion of between about 0.1 and 2% (by weight of the dry pulp solids),advantageously from between about 0.2 and 1%, and preferably between about 0.2 and 0.4 weight percent.
  • the pulp slurry can be intended for tissue production, disposable diaper production, or any other cellulosic fiber product wherein reduced tensile strength is desired.
  • the pulp slurry will be fluffed for production of disposable diapers, sanitary absorbents, and the like.
  • the sheets were removed from the mold and pressed between dry blotters at a pressure of 3.5 kg/cm 2 (50 psi) for a period of 5 minutes on a first press followed by 2 minutes on a second press.
  • the pressed sheets then were placed in TAPPI drying ring which were housed under standardized conditions of a constant temperature of 21.1 0 C (70°F) and 50% relative humidity for drying overnight.
  • the conditioned hand sheets were tested in accordance with standard test methods set forth below :
  • the debonders were added to the pulp at the rate of 1.5 g per kilogram of pulp.
  • the pulp was softwood Kraft pulp (Albacel) for the first text series and softwood sulfite pulp (Puget S) for the second test series. The following test results were recorded.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Paper (AREA)
  • Sanitary Thin Papers (AREA)
  • Absorbent Articles And Supports Therefor (AREA)
EP84630017A 1983-02-10 1984-02-08 Composition déliante pour fibres comprenant un composé diamido-ammonium quaternaire et un acide gras alkoxylé Withdrawn EP0116512A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US46555383A 1983-02-10 1983-02-10
US465553 1983-02-10

Publications (1)

Publication Number Publication Date
EP0116512A1 true EP0116512A1 (fr) 1984-08-22

Family

ID=23848274

Family Applications (1)

Application Number Title Priority Date Filing Date
EP84630017A Withdrawn EP0116512A1 (fr) 1983-02-10 1984-02-08 Composition déliante pour fibres comprenant un composé diamido-ammonium quaternaire et un acide gras alkoxylé

Country Status (3)

Country Link
EP (1) EP0116512A1 (fr)
JP (1) JPS59163499A (fr)
PT (1) PT78086B (fr)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5552020A (en) * 1995-07-21 1996-09-03 Kimberly-Clark Corporation Tissue products containing softeners and silicone glycol
WO1997049858A1 (fr) * 1996-06-25 1997-12-31 Ildiko Tanczos Procede de production de pate chimique/cellulose
US5730839A (en) * 1995-07-21 1998-03-24 Kimberly-Clark Worldwide, Inc. Method of creping tissue webs containing a softener using a closed creping pocket
US6156157A (en) * 1995-07-21 2000-12-05 Kimberly-Clark Worldwide, Inc. Method for making soft tissue with improved bulk softness and surface softness
US6379498B1 (en) 2000-02-28 2002-04-30 Kimberly-Clark Worldwide, Inc. Method for adding an adsorbable chemical additive to pulp during the pulp processing and products made by said method
US6582560B2 (en) 2001-03-07 2003-06-24 Kimberly-Clark Worldwide, Inc. Method for using water insoluble chemical additives with pulp and products made by said method
US7749356B2 (en) 2001-03-07 2010-07-06 Kimberly-Clark Worldwide, Inc. Method for using water insoluble chemical additives with pulp and products made by said method
WO2015165783A1 (fr) * 2014-04-28 2015-11-05 Mondi Ag Cellulose modifiée

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4531503B2 (ja) * 2004-09-17 2010-08-25 花王株式会社 紙質向上剤

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1030396A (en) * 1963-04-26 1966-05-25 I C I Organics Inc Bis-acyl-dialkylene triamines
US3677886A (en) * 1968-12-27 1972-07-18 Korsnaes Marma Ab Method of producing highly absorbent cellulose
DE2254120A1 (de) * 1972-11-04 1974-05-16 Pelz & Co Kg W Sauggaehiges fasermaterial fuer hygienische und medizinische zwecke
US4144122A (en) * 1976-10-22 1979-03-13 Berol Kemi Ab Quaternary ammonium compounds and treatment of cellulose pulp and paper therewith
FR2431569A1 (fr) * 1978-07-21 1980-02-15 Kenogard Ab Procede pour la fabrication de pate pour duvet
US4233164A (en) * 1979-06-05 1980-11-11 The Proctor & Gamble Company Liquid fabric softener
EP0049924A1 (fr) * 1980-10-15 1982-04-21 THE PROCTER & GAMBLE COMPANY Procédé de fabrication d'un tissu de papier souple et absorbant et papier ainsi préparé

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1030396A (en) * 1963-04-26 1966-05-25 I C I Organics Inc Bis-acyl-dialkylene triamines
US3677886A (en) * 1968-12-27 1972-07-18 Korsnaes Marma Ab Method of producing highly absorbent cellulose
DE2254120A1 (de) * 1972-11-04 1974-05-16 Pelz & Co Kg W Sauggaehiges fasermaterial fuer hygienische und medizinische zwecke
US4144122A (en) * 1976-10-22 1979-03-13 Berol Kemi Ab Quaternary ammonium compounds and treatment of cellulose pulp and paper therewith
FR2431569A1 (fr) * 1978-07-21 1980-02-15 Kenogard Ab Procede pour la fabrication de pate pour duvet
US4233164A (en) * 1979-06-05 1980-11-11 The Proctor & Gamble Company Liquid fabric softener
EP0049924A1 (fr) * 1980-10-15 1982-04-21 THE PROCTER & GAMBLE COMPANY Procédé de fabrication d'un tissu de papier souple et absorbant et papier ainsi préparé

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5552020A (en) * 1995-07-21 1996-09-03 Kimberly-Clark Corporation Tissue products containing softeners and silicone glycol
US5730839A (en) * 1995-07-21 1998-03-24 Kimberly-Clark Worldwide, Inc. Method of creping tissue webs containing a softener using a closed creping pocket
US6156157A (en) * 1995-07-21 2000-12-05 Kimberly-Clark Worldwide, Inc. Method for making soft tissue with improved bulk softness and surface softness
WO1997049858A1 (fr) * 1996-06-25 1997-12-31 Ildiko Tanczos Procede de production de pate chimique/cellulose
US6379498B1 (en) 2000-02-28 2002-04-30 Kimberly-Clark Worldwide, Inc. Method for adding an adsorbable chemical additive to pulp during the pulp processing and products made by said method
US6582560B2 (en) 2001-03-07 2003-06-24 Kimberly-Clark Worldwide, Inc. Method for using water insoluble chemical additives with pulp and products made by said method
US7749356B2 (en) 2001-03-07 2010-07-06 Kimberly-Clark Worldwide, Inc. Method for using water insoluble chemical additives with pulp and products made by said method
US7993490B2 (en) 2001-03-07 2011-08-09 Kimberly-Clark Worldwide, Inc. Method for applying chemical additives to pulp during the pulp processing and products made by said method
WO2015165783A1 (fr) * 2014-04-28 2015-11-05 Mondi Ag Cellulose modifiée

Also Published As

Publication number Publication date
PT78086B (en) 1986-04-17
PT78086A (en) 1984-03-01
JPS59163499A (ja) 1984-09-14

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Inventor name: ZEMAN, WILLIAM JOHN